This
study demonstrates a sustainable catalytic
CO2 conversion to near 100% CO selectivity at ambient pressure
on In2O3. Critically, high CO yield could be
observed at the cost of undesired methanation, using a lower than
stoichiometric amount of hydrogen in the feed; 1:1 and 1:0.67 CO2:H2 ratios exhibit 98–99.6% CO selectivity
with 25–38% CO2 conversion between 773 and 873 K.
CO2 and H2 conversion under steady-state conditions
at 773–873 K suggests a 1:1 ratio of adsorbed reactants (with
1:0.67 CO2:H2 feed) on the catalyst surface,
underscoring the presence of an ideal reactant composition for the
reverse water-gas shift reaction, while H2-rich feed compositions
show the H2-dominated surface. Surface electronic structure
changes, under near-operating conditions, were explored with near
ambient pressure photoelectron spectroscopy (NAPPES), and the interesting
findings are as follows: (a) A shift in the valence band to lower
binding energy, up to 0.6 eV, was observed because of electron filling
at high temperatures. (b) An observation of heterogeneous nature of
the catalyst surface under NAPPES measurement conditions is attributed
to the generation of active oxygen vacancy (Ov) sites,
which in turn changes the work function of In2O3. (c) The above changes are found to be reversible, when the reaction
was stopped. Vibrational features of the reactant molecules were observed
to be broadened in the active temperature window of the catalyst supporting
the heterogeneous character of the catalyst surface because of dynamic
Ov generation. By optimizing gas hourly space velocity,
CO2:H2 ratio, and reaction temperature, exclusive
CO selectivity is possible with a H2:CO2 ratio
of ∼0.67, which will avoid the product separation stage altogether,
while minimizing the expensive H2 in the reactant feed.